WO2004078812A1 - (co)polymere sequence, composition de copolymere sequence pour la modification d'asphalte, leur procede de production et composition d'asphalte - Google Patents

(co)polymere sequence, composition de copolymere sequence pour la modification d'asphalte, leur procede de production et composition d'asphalte Download PDF

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Publication number
WO2004078812A1
WO2004078812A1 PCT/JP2004/001923 JP2004001923W WO2004078812A1 WO 2004078812 A1 WO2004078812 A1 WO 2004078812A1 JP 2004001923 W JP2004001923 W JP 2004001923W WO 2004078812 A1 WO2004078812 A1 WO 2004078812A1
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Prior art keywords
polymer
block
asphalt
weight
composition
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PCT/JP2004/001923
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English (en)
Japanese (ja)
Inventor
Masatoshi Torii
Hiroshi Kato
Masato Suzuki
Takumi Miyachi
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Kraton Jsr Elastomers K.K.
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Application filed by Kraton Jsr Elastomers K.K. filed Critical Kraton Jsr Elastomers K.K.
Priority to BRPI0407647-8A priority Critical patent/BRPI0407647A/pt
Priority to EP04712739A priority patent/EP1602673A4/fr
Priority to CA2517142A priority patent/CA2517142C/fr
Priority to US10/545,552 priority patent/US20060229391A1/en
Priority to AU2004218190A priority patent/AU2004218190B9/en
Publication of WO2004078812A1 publication Critical patent/WO2004078812A1/fr

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    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L95/00—Compositions of bituminous materials, e.g. asphalt, tar, pitch
    • C08L95/005—Aqueous compositions, e.g. emulsions
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F297/00—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer
    • C08F297/02—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the anionic type
    • C08F297/04—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the anionic type polymerising vinyl aromatic monomers and conjugated dienes
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L53/00—Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
    • C08L53/02—Compositions of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers of vinyl-aromatic monomers and conjugated dienes
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00—Polymer mixtures characterised by other features
    • C08L2205/02—Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group

Definitions

  • Block (co) polymer Block (co) polymer, block copolymer composition for asphalt modification, method for producing the same, and asphalt composition
  • the present invention relates to: 1) an aromatic vinyl compound having a specific structure, or a block (co) polymer of this with a conjugated diene, more particularly a block of an asphalt-modifying block (co) polymer or a composition thereof A block (co) polymer suitable as a compatibilizer capable of improving the solubility in asphalt, 2) a block copolymer comprising this block (co) polymer and a block copolymer for asphalt modification Asphalt-modified block copolymer composition excellent in solubility in asphalt, 3) Method for producing this composition, and 4) the above-mentioned block copolymer composition for asphalt modification Phase separation safety during storage, obtained by blending into straight asphalt, aromatic hydrocarbon resin and heavy oil, or Excellent stability (hereinafter referred to as storage stability), low viscosity, excellent processability and handleability, and further excellent softening point, elongation, toughness, tenacity, etc.
  • storage stability Excellent stability
  • the present invention relates to a composition, for example, a highly viscous modified asphalt composition suitable for drainage / low noise pavement.
  • asphalt is inexpensive and easily available, and is widely used for road paving, waterproofing, soundproofing sheets, damping materials, and so on.
  • Storage stability is a phenomenon in which the performance, for example, the softening point, decreases as a whole, or phase separation occurs during storage, resulting in a difference between the upper layer and the lower layer.
  • binder physical properties such as asphalt softening point and toughness / tenacity are considerably improved, storage stability at high temperature is not necessarily sufficient.
  • a method is used to increase the softening point and toughness / tenacity and secure the balance of elongation by increasing the addition amount of the block copolymer to the high molecular weight copolymer.
  • the present invention is excellent in solubility in asphalt by highly controlling the molecular structure, and when made into an asphalt composition, is excellent in storage stability at high temperature, and further has a low melt viscosity, It is an object of the present invention to provide an asphalt composition excellent in the above, and further to provide an asphalt composition that can be used for road pavement, waterproof sheet and the like. Disclosure of the invention
  • the present invention relates to a block (co) polymer having one or more aromatic burle polymer blocks as its essential component and a polymer block mainly composed of this and one or more conjugated dienes.
  • the content of the vinyl bond in the polymer block B as a main component is 10 to 50% by weight, and the weight average molecular weight of the polymer block S is 500 to 200,000, and the polymer block S
  • the present invention relates to a block (co) polymer (hereinafter also referred to as “(i) block (co) polymer”) wherein the total amount of weight average molecular weight of + S ′ is 1,000 to 30,000.
  • the weight average molecular weight of the whole block (co) polymer is preferably 5,000 to 50,000.
  • the content be 10% by weight or more and less than 100% by weight.
  • the present invention provides the above-mentioned (i) block (co) polymer,
  • a block copolymer comprising a polymer block mainly composed of at least two aromatic vinyl compounds and a polymer block mainly composed of at least one conjugated gene, which is a block copolymer represented by the general formula (II) S— B— S, general formula (III) S— B— S ′ and Z or general formula (IV) (SB) 2 — X [—in general formula (II) to (!
  • V), S, S ′ , B is the same as in the general formula (I), and X is a coupling agent residue], and the total content of the bound vinyl aromatic compound in the block copolymer is 20 to 70% by weight, 10 to 50 weight of vinyl bond content in polymer block B mainly composed of / 0 , and a block copolymer having a weight average molecular weight of the polymer block S of 10,000 to 200,000, and a weight average molecular weight of the polymer block S 'of 10,000 to 200,000 (Hereafter, it is also referred to as “(mouth) block copolymer”)
  • the present invention relates to a combined composition.
  • the molecular weight of the (b) block (co) polymer peak determined by gel permeation chromatograph (GPC) is 1/80 to 1 Z 3 of the molecular weight of the (mouth) block copolymer peak. It is preferable to correspond to less than.
  • the present invention separately polymerizes the above (i) block (co) polymer and (port) block copolymer in an inert hydrocarbon solvent using an organic lithium compound as an initiator in a solution polymerization method.
  • the present invention also relates to a method for producing an asphalt-modifying block copolymer composition obtained by dissolving and dissolving each of the obtained polymer solutions and then dissolving them.
  • the present invention is a production method of simultaneously polymerizing (i) block (co) polymer and (mouth) block copolymer, wherein the organic lithium compound is initiated in an inert hydrocarbon solvent.
  • an aromatic vinyl compound and a conjugated diene are sequentially polymerized in a polymerization step, and at least an initiator is used.
  • the present invention relates to a method for producing an aromatic vinyl compound, and an aromatic vinyl compound, a propylene glycol modifying plug composition for at least one insertion of a conjugated diene.
  • the present invention relates to an asphalt composition (hereinafter referred to as "asphalt composition (1) J") contained.
  • the present invention provides the above block copolymer composition, a sulfate asphalt, an aromatic hydrocarbon resin, and a heavy oil with respect to 100 parts by weight of a straight asphalt. 1 to 20 parts by weight, 0 to 40 parts by weight of aromatic hydrocarbon resin, 0 to 40 parts by weight of heavy oil, and the total of aromatic hydrocarbon resin and heavy oil is 1 to
  • the present invention relates to an asphalt composition (hereinafter also referred to as "asphalt composition (2)") which is contained in a proportion of 60 parts by weight.
  • FIG. 1 is a chart showing the molecular weight distribution of the block copolymer used in Example 1 according to gel permeation chromatography.
  • the horizontal axis is molecular weight (log molecular weight), and the vertical axis is molecular weight distribution (% by weight).
  • Fig. 2 is a photomicrograph showing that the asphalt phase and the polymer phase were compatible and that the sea-island structure was single-phased in the asphalt composition of Example 1, and that of the composition of Comparative Example 2 was separated. The photomicrograph of as it is is shown.
  • FIG. 3 is a chart showing a molecular weight distribution by gel permeation chromatography of the block copolymer used in Example 3.
  • the horizontal axis is molecular weight (log molecular weight), and the vertical axis is molecular weight distribution (% by weight).
  • the (i) block (co) polymer used in the present invention is essentially a polymer block S and / or S 'mainly composed of an aromatic vinyl compound, and a polymer block mainly composed of this and a conjugated diene A block (co) polymer sometimes containing B, wherein the (mouth) block copolymer is a polymer block mainly composed of an aromatic boule compound S and / or S, a weight mainly composed of a conjugated diene It is a block (co) polymer consisting of coalesced block B. 3
  • an aromatic bule compound used to obtain (i) block (co) polymer or (mouth) block copolymer styrene, t-butylstyrene, ct-methinolestyrene, p-methylstyrene, dibiphenyl
  • ninobenzene 1,1-diphenylstyrene, N, N-dimethinole p-aminoethynolestyrene, N, N-jetyl p-amino-ethylstyrene, burylpyridine and the like, with particular preference being given to styrene, ⁇ -methylstyrene Is preferred.
  • the block (co) polymer essentially comprises a polymer block mainly composed of an aromatic vinyl compound as described above, and a block which may contain a polymer block mainly composed of a conjugated diene and the polymer block (co )
  • a polymer which is essentially a polymer block mainly composed of one or more aromatic vinyl compounds, and may sometimes contain a polymer block mainly composed of one or more conjugated dienes
  • General formula (I) (S- ⁇ ) m -s' eta [In formula (I), s and s are polymer blocks having an aromatic vinyl compound as a main component, and B is a heavy component having a conjugated gene as a main component
  • m and n are integers of 0 or 1
  • m + n 1 or more.
  • the (i) block (co) polymer of the present invention is not Although it exhibits sufficient performance as a reforming effect, it has greatly improved the solubility of asphaltphas modifiers in asphalt, which were not suitable for practical use due to problems with handling such as processability and storage stability. And are suitable as these compatibilizers because they have the effect of compensating for the above-mentioned disadvantages.
  • -(I) Total bound aromatic vinyl compound content in the block (co) polymer is 1
  • the vinyl bond content of polymer block B mainly composed of a conjugated diene in (i) block (co) polymer is 10 to 50% by weight. If the content is less than 10% by weight, the compatibility effect is lowered and it is difficult to obtain due to the nature of the reaction in the method of producing the (co) polymer, which is not preferable. On the other hand, if it exceeds 50% by weight, the low temperature properties of the assufalto composition tend to be poor, and the compatibility effect becomes insufficient, so that the dissolution time becomes long, the storage stability is poor and it is not preferable. Preferably, it is 12 to 40% by weight.
  • the weight average molecular weight of the polymer block S (polymer block mainly composed of an aromatic vinyl compound) in the (i) block (co) polymer is 500 to 20, 00, and The total amount of weight average molecular weight of the polymer block S + S 'is 1, 0 0 0 to 3 0, 0 0 0.
  • the improvement effect of the (mouth) block copolymer is Insufficient, especially the dissolution time to asphalt is extremely long, and the improvement of storage stability can not be seen.
  • the weight average molecular weight of the polymer block S is less than 500 and / or the total amount of S + S 'is less than 1000, the dissolution time will be shorter and the viscosity will be lower. Although the processability becomes easy, the softening point and toughness / tenacity of the asphalt composition are insufficient, which is not preferable.
  • the weight average molecular weight of the (i) block (co) polymer as a whole is preferably 5, 000 to 50, 0 0 0. If it is less than 500, the dissolution time is short and the viscosity is low, so the effect on the processability can be obtained, but the softening point of the asphalt composition is insufficient, while 50, 0 0 0 When it exceeds, the improvement effect of the (mouth) block copolymer is insufficient, and in particular, the dissolution time in asphalt becomes long, which is not preferable.
  • the polymer block represented by B in the general formula (I) is mainly composed of a conjugated diene, but may contain an aromatic boule compound or the like.
  • the bound aromatic vinyl compound can be contained in an amount of 0 to 40% by weight, and more preferably 0 to 30% by weight, of the total bound aromatic boule compound in (i).
  • the structure may be random or tapered taper blocks.
  • the (mouth) block copolymer used for the composition for asphalt modification of the present invention is: .S--B--S, S--B--S 'or (S--B) 2 X (S, S', B) Is the same as in general formula (I), and X is a coupling agent residue.
  • the total bond content of the aromatic vinyl compound in the (mouth) block copolymer is 20 to 70% by weight. If the total bond content is less than 20% by weight, the softening point, the toughness and the tenacity become insufficient, and the flow resistance deformation resistance at high temperatures also becomes insufficient. On the other hand, if it exceeds 70% by weight, the penetration of the quick composition becomes so small that the low temperature elongation is lowered. Preferably, it is 20 to 50% by weight.
  • (polymer) polymer block mainly composed of conjugated gen in the block copolymer
  • vinyl bond content is 10 to 50 weight. / 0 Those having a boule bond content of less than 10% by weight are difficult to obtain in the production method. On the other hand, if it exceeds 50% by weight, the penetration of the fast composition becomes small and the low temperature elongation decreases. Preferably, it is 12 to 45% by weight.
  • S and B in S--B--S, S--B--S 'or (S--B) 2 X which are (mouth) block copolymers used in the composition for modifying asphalt of the present invention
  • the weight average molecular weight of S '(a polymer block composed mainly of an aromatic vinyl compound) is preferably 10, 000 to 20, 000, more preferably 12, 200 to 1: 8 000. .
  • the weight average molecular weight is less than 10,000, the softening point and toughness' tenacity of the resulting asphalt composition are insufficient, and the decrease in flow resistance is also large, which is not preferable.
  • more than 20,000 In other words, (i) the solubility of the polymer significantly deteriorates even under the presence of the block (co) polymer, and the storage stability may be further deteriorated to cause phase separation.
  • the block B mainly composed of a conjugated gen may contain an aromatic burle compound as in (i).
  • the bound aromatic vinyl compound can be contained in an amount of 0 to 40% by weight of the total bound aromatic vinyl compound in (mouth), more preferably 0 to 30% by weight.
  • the structure may be a random shape or a tapered block that gradually increases.
  • the aromatic vinyl compound bound to the B block mainly composed of a conjugated gen it is possible to control the compatibilizing effect by adjusting the chain length of s (and ⁇ ⁇ ⁇ or B and B.) B block
  • the amount of the bound aromatic vinyl compound exceeds 40% by weight, the molecular weight of the S (and / or S ') block becomes too small, and the compatibilizing effect becomes insufficient, which is not preferable.
  • It may be a tapered block in which this gradually increases.
  • the weight average molecular weight of the (mouth) block copolymer is preferably 60, 000 to 400,000, more preferably 100, 000 to 300, 000, and particularly preferably 120, 00 to 300, It is 000. If this molecular weight is less than 60,000, the softening point and toughness' tenacity of the resulting asphalt composition are insufficient, and the decrease in flow resistance is also large, which is not preferable. on the other hand,
  • the melt flow rate (G method of JIS K 7210), which is an index of fluidity, is preferably 0 to 3 0, more preferably 0.01 to 15 and particularly preferably 0.01 to 10.
  • the (i) block (co) polymer used in the present invention is obtained, for example, by sequential polymerization of an aromatic vinyl compound and a conjugated diene using an organic lithium compound or the like as a polymerization initiator in an inert hydrocarbon solvent. It can be manufactured by For example, first, an aromatic vinyl compound is polymerized and then a conjugated gene is polymerized to stop the reaction, or further, an aromatic vinyl compound and a conjugated gen compound are sequentially inserted, and the reaction is stopped when the desired structure is obtained. It will come out to manufacture. In addition, in the polymerization of a conjugated diene, a desired amount of an aromatic vinyl compound may be added and copolymerized as required.
  • an (oral) block copolymer may be prepared, for example, using an organic lithium compound or the like as a polymerization initiator in an inert hydrocarbon solvent, and first polymerizing an aromatic boule compound and then polymerizing a conjugated diene. It can be produced by reacting a coupling agent or by reacting an aromatic vinyl compound again.
  • a desired amount of an aromatic butyl compound may be added and copolymerized as necessary.
  • hydrocarbons such as pentane, n-hexane, heptane, octane, methylolecyclopentane, cyclohexane, benzene, xylene and the like are used, and among these, cyclohexane is preferable.
  • organoaluminum compound which is a polymerization initiator an organolithium compound is preferable.
  • organic lithium compound organic monolithium, organic di Lithium and organic polylithium compounds are used.
  • acetyl lithium n-propyl lithium, iso-propyl lithium, n-butyl lithium, sec-butyl lithium, isoprenyl dilithium and the like, and it is 0.2 to 2 parts by weight per 0 parts by weight of monomers. Used in part quantities.
  • a Lewis base as a regulator of the micro structure, ie, the content of boule bond of conjugated gen moiety, for example, ether, jamin etc., specifically, dimethyl ether ⁇ , tetrahydrofuran, propizoleete ⁇ , butinole ethenole, high grade Ethers, Ether derivatives of polyethylene glycols such as ethylene glycol butyl ether phenol, diethylene glycol dimethyl ether alcohol, diethylene glycol dimethyl ether ether, triethylene glycol alcohol butyl ether, ethylene glycol carboxyl ester, etc.
  • Examples of hammins include tetramethyldiimidazole, tertiary amines such as pyridine and tributylamine, and the like, which are used together with an inert hydrocarbon solvent.
  • the polymerization reaction is usually carried out at 20 to 120 ° C, preferably 30 to 100 ° C. Also, the polymerization may be carried out at a controlled temperature or may be carried out at an elevated temperature without heat removal.
  • a bifunctional coupling agent used for the (co) block copolymer
  • a bifunctional coupling agent is used.
  • Dichloromethane Tanor, etc., Dichlorosilane, Dichlorosilane, Methinodichlorosilane, Dimethy / Resichlorosilane, Monoeth / Resichlorosilane, Jetyldichlorosilane, Monobutyl Dichlorosilane Silane, Diptinoridichlorosilane, Mono Hexanoic resin chlorosilane, dihexyl dichlorosilane, dipromosilane, monomethyone di-mouth mosilane, di-methyone di-bi halides such as di-molybdenum mosilane, divinyl / madzene, di-vinyl aromatic compounds such as di-vinyl naphthalene, formate ethyl, acetate ethyl , Ethyl acetate such as methyl acetate, methyl propionate, phenyl acetate, ethyl
  • (I) Conjugated amount of the aromatic vinyl compound in the block (co) polymer and (mouth) block copolymer is controlled by the amount of monomer supplied at the time of polymerization in each step, and is controlled as necessary
  • the burle binding content of gen is adjusted by varying the components of the mik mouth regulator described above.
  • the structure of the aromatic boule compound / conjugated diene of the polymer block mainly composed of the conjugated diene is also adjusted by the above-mentioned microregulatory agent.
  • the structural control of the aromatic vinyl compound Z-conjugated is to control the bonding state such as the random, tapered, or block structure of the aromatic boule compound bonded to the coagent.
  • the weight average molecular weight of the block (co) polymer of (i) to (mouth) is controlled by the addition amount of a polymerization initiator, for example, sec.
  • the asphalt-modifying composition of the present invention comprises the above-mentioned (mouth) block copolymer as a main component, and further contains a (i) block (co) polymer as a compatibilizer.
  • the weight ratio of the (i) component to the (mouth) component in this composition is 10-40 / 90-60. If the weight ratio of the component (b) is less than 10, the effect on solubility is insufficient, while if it is more than 40, the physical properties of the binder become insufficient. Preferably, it is 1 to 30/90 to 70.
  • the molecular weight of the peak of (i) block (co) polymer which is measured by gel permeation chromatography (GPC) is Those corresponding to 1/80 to less than 1/3 of the molecular weight of the coalescing peak are preferred. If this value is less than 1/80, the asphalt softening point becomes insufficient due to the molecular weight being too low, and the compatibilizing effect can not be sufficiently obtained, which is not preferable.
  • the ratio of peaks is the ratio of the highest peak (main peak) among a plurality of peaks of each block copolymer.
  • (i) block (co) polymer, and (mouth) block copolymer are added in a hydrocarbon solvent as a solution weight using an organic lithium compound as an initiator. It is preferable to obtain each of the polymer solutions obtained by legally polymerizing separately, mixing and homogenizing the obtained respective polymer solutions, and then desolvating. For example, After the (mouth) block copolymer is produced as described above, the above (i) block (co) polymer solution may be mixed with solution, homogenized, and then dissolved to dissolve. .
  • the (i) component can also be finished independently using a special production method.
  • production facilities generally used for force (mouth) block copolymers etc. the problem of stickiness and poor drying can be obtained. It can not be practically manufactured.
  • block copolymer composition of the present invention can be produced by simultaneously polymerizing the (i) block (co) polymer with the polymerization of the (opening) block copolymer described above.
  • the general formula of (i) block (co) polymer is limited to the S-B structure
  • the general formula of the (b) block copolymer is limited to the S-B-S structure etc.
  • the aromatic vinyl compound and the polymerization initiator (initiator 1) are brought into contact and reacted, and then a conjugated diene is added, After the reaction is substantially complete, a polymerization initiator (initiator 1) is added, and a conjugated agent is added again to continue the production of the (mouth) block copolymer, (i) block (co) Start the production of the polymer. Finally, an aromatic vinyl compound may be reacted to produce (b) and (b) a block copolymer simultaneously to form a composition.
  • the addition of the second stage initiator is preferably after the completion of the polymerization of the first stage conjugated diene, but the adjustment of the first stage comonomer addition amount is preferable. However, it may be added in the middle of the polymerization, and the addition of the second stage of the conjugated gene may be omitted.
  • the asphalt composition (1) of the present invention is a composition containing the above-mentioned composition for modifying asphalt and straight asphalt.
  • the asphalt asphalt composition (1) The straight asphalt used is obtained as a residue after subjecting an asphalt-based crude oil to atmospheric distillation and steam or vacuum distillation. Since Stratosphalt is easy to dissolve the block copolymer composition of the present invention, it is easy to process and handle.
  • the straight asphalt preferably has a penetration of 50 to 200. If the needle penetration is less than 50, flexibility at low temperature tends to be impaired, while if it exceeds 200, abrasion resistance and flow resistance tend to be lowered.
  • the weight ratio of modifying block copolymer composition to straight phasphalt in the asphastoal composition (1) is 2 to 15/98 to 85, preferably 3 to 13/97 to 8 7 If the weight ratio of the modifying block copolymer composition is less than 2, the asphalt modifying effect can not be seen, the softening point is insufficient, and the penetration and toughness' tenacity are low. On the other hand, if it exceeds 15, the softening point and toughness' tenacity are sufficient, but the dissolution time to asphalt becomes extremely long, Compatibility is also worse. In addition, the melt viscosity of the asphalt composition becomes extremely high, which makes processing and handling difficult.
  • the modifying block copolymer composition of the present invention can usually be used in the form of pellet, chromium, powder or the like.
  • the asphalt composition (2) is a composition containing the composition for modifying asphalt and the same asphalt as described above, an aromatic hydrocarbon resin, and / or a heavy oil. is there.
  • the aromatic hydrocarbon resin refers to a resin including rosin and its derivative, terpene resin, petroleum resin and its derivative, coumarone resin, alkylphenol resin, alkyd resin and the like.
  • Heavy oil refers to vegetable oil such as rice bran oil and soybean oil, animal oil such as fish oil and soy sauce, petroleum-based heavy hydrocarbon oil such as cylinder oil and lubricating oil, but from an economic point of view It is preferable to use petroleum-based heavy hydrocarbon oil, especially aromatic process oil.
  • the blending ratio of the asphalt composition (2) is 1 to 20 parts by weight, preferably 3 to 18 parts by weight of the asphalt-modifying composition with respect to 100 parts by weight of the above asphalt. 0 to 40 parts by weight of a hydrocarbon-based hydrocarbon resin, 0 to 40 parts by weight of heavy oil and 1 to 60 parts by weight of a total of aromatic hydrocarbon resin and heavy oil, preferably 5 40 parts by weight.
  • the blending amount of the composition for asphalt modification is less than 1 part by weight, the modifying effect of the asphalt is not observed, the softening point is insufficient, and the penetration and the toughness ⁇ tenacity are low. Above 20 parts by weight, the softening point, toughness' tena The city is sufficient but the dissolution time to asphalt is significantly longer and the compatibility is worse. In addition, the melt viscosity of the asphalt composition becomes extremely high, which makes processing and handling difficult.
  • Asphastoal compositions (1) to (2) of the present invention can be prepared by adding the above-mentioned block copolymer composition for modification or the aromatics to straight asphalt under stirring which is usually heated and melted at 140 to 190 ° C. It is manufactured by charging and mixing a hydrocarbon-based hydrocarbon resin and / or heavy oil.
  • styrene-butadiene-styrene block copolymers and styrene-isoprene-styrene block copolymers can be used in combination with the asphalt compositions (1) to (2) of the present invention.
  • other thermoplastic elastomers or thermoplastic resins such as styrene-butadiene rubber latex, ethylene-vinyl acetate copolymer, ethylene-acrylic acid ethyl copolymer, atactic polypropylene, 1,2-polybutadiene
  • other polymers such as ethylene-propylene rubber can be used in combination.
  • fillers such as silica, talc and calcium carbonate, pigments, anti-aging agents, crosslinking agents, flame retardants, etc. Additives can be blended. In addition, when used for road pavement, it is possible to add gravel etc.
  • the peak molecular weight was calculated from the chromatograph obtained above by preparing a calibration curve using standard polystyrene (manufactured by Shell Chemical Co. Ltd (US)). Also, the content was similarly calculated from the area ratio of each component of the chromatograph.
  • Automelt Indexer 1 (TP-404 type) manufactured by Tester Sangyo Co., Ltd. was used.
  • the analysis sample measured the said composition according to G method (200 degreeC, 5 kg load) of JIS-K7210.
  • Dissolution time A during preparation of the asphalt composition, a small amount of the content is collected during asphalt mixing, applied on a polyester (Tetron) sheet, and visually observed, until solid particles of block copolymer are not recognized. It was time for.
  • the asphalt composition was evaluated based on the samples judged to be dissolved by the dissolution time A, and the performance was judged.
  • the phase structure of the asphalt and polymer in the Miku mouth region is important Found out that the As determined by the dissolution time A, it has been found that storage stability as an asphalt composition is particularly poor when phase separation is observed in the micro area even in the dissolved composition.
  • the condition of forming a single phase in the micro area is essential in order to fully demonstrate product performance as an asphalt composition and to prevent variation in quality. It has As mentioned above, evaluation by the following dissolution time B was performed.
  • the dissolution time B was as follows.
  • the asphalt phase and the polymer phase be uniformly dispersed and that the sea-island structure exhibit a single phase, as described above.
  • combinations of substantially incompatible systems did not form a single phase even after mixing for more than 15 hours.
  • a composition which does not form a single phase even by stirring for 8 hours or more can not be put to practical use, and it is representative of storage stability even if semi-forced mechanical mixing is carried out to produce an asphalt composition. Performance is insufficient.
  • the mixing time was uniformly 8 hours including the examples, and the following physical property measurement was also performed for 8 hours.
  • the mixture of Asphalt in this test is poured into a container made of an aluminum can, and after standing still in a nitrogen atmosphere at 180 ° C. for 72 hours in an oven, it is cooled at room temperature, and the aluminum can is at the upper middle and lower portions. Divided into three. The following evaluations were made on the upper and lower samples excluding the central part.
  • FIG. 1 A chart showing a molecular weight distribution of this block copolymer composition by gel permeation chromatography is shown in FIG.
  • Example 2 Examples 2, 5 to 7, 13 15, 15 16, 16, 20, 23, 24 As in Example 1 except that the loadings of styrene, 1,3-butadiene, sec-butyrene lithium are changed Then, a block copolymer shown in Table 1 and a block copolymer composition for asphalt modification were obtained, an asphalt composition was prepared, and its performance was evaluated. Table 1 shows the evaluation results of each property.
  • the block copolymer is a stainless steel polymerization vessel similar to Example 1. 50 kg of hexene hex, 1. 2 g of ethylene glycol coletinoleate tenoleate and 1.2 kg of styrene are prepared. Bring warm water to the jacket, bring the contents to 40 ° C, then add 6 g of sec-butyllithium to start polymerization, and after completion of styrene polymerization, put cold water in the jacket so that the contents temperature will be 80 ° C. The mixture was slowly added with 1, 3-butadiene 5.
  • FIG. 3 is a chart showing the molecular weight distribution of this block copolymer composition by gel permeation chromatography.
  • the block copolymer was produced as follows. That is, in a stainless steel polymerization vessel similar to that of Example 1, hexene 2O kg in hexane and 0.45 kg in styrene were charged, and the contents were heated to 40 ° C. by passing hot water through a jacket.
  • the (mouth) block copolymer was polymerized in the same manner as in Example 1 except that the amounts of styrene, 1,3-butadiene, sec-butyl lithium and ethylenedaryl glycol ether were changed.
  • the block copolymer shown in Table 1 was obtained, and the same operation as in Example 1 was carried out to obtain a block copolymer composition and an asphalt composition, and their performances were evaluated. Table 1 shows the evaluation results of each property.
  • Example 8 In a polymerization vessel used in Example 1, 5 kg of cyclohexane and 0.8 kg of styrene were charged, and the contents were brought to 40 ° C. by passing hot water through a jacket.
  • This polymerization solution was steam stripped as in Example 1, and the obtained polymer was dried to obtain a block copolymer composition, and its performance was evaluated.
  • Table 1 shows the evaluation results of each property.
  • Example 1 In a polymerization vessel used in Example 1, 20 kg of cyclohexane and 0.3 kg of styrene were charged, the contents were heated to 40 ° C. by passing warm water into a jacket, and then 6 g of sec-butyl lithium was added. Start polymerization, and after completion of polymerization of styrene, while passing cold water through the jacket so that the content temperature is 80 ° C, 1.3 kg of 1,3-butadiene and 0.3 kg of 0.3 kg of styrene three times Divided evenly, and added slowly and evenly. After the polymerization was completed, 3 ml of methanol was added, and the mixture was stirred for 10 minutes to obtain (i) a block copolymer. Thereafter, in the same manner as in Example 1, a (bread) block copolymer is obtained, an asphalt composition is prepared, and the performance thereof is obtained. Was evaluated. Table 1 shows the evaluation results of each property.
  • Example 1 In a polymerization vessel used in Example 1, 20 kg of cyclohexane, 8 g of ethylene glycol monoethyl ether, 8 mg of ethylene glycol, and 0.4 kg of styrene were charged, the contents were brought to 40 ° C. by passing warm water through a jacket, and then The polymerization is started by adding 5 g of sec-butyl lithium, and after completion of the polymerization of styrene, while passing cold water through the jacket so that the content temperature becomes 80 ° C., 1,3-butadiene 1.38 At the same time, 0.8 g of styrene and 0.2 g of styrene were simultaneously added slowly and almost completely polymerized.
  • Example 10 In the polymerization of the block copolymer, all of Example 10 and Example 10 were changed except that the charge amounts of styrene, 1,3-butadiene, sec-butynore lithium and ethyleneglacinoregetinoreatenore were changed. In the same manner, a block copolymer composition and an asphalt composition were obtained, and their performances were evaluated. Table 1 shows the evaluation results of each property.
  • Example 4 In the same manner as in Example 4 except that the amounts of styrene, 1,3-butadiene and sec-butyllithium were changed, the block copolymer shown in Table 2 and the block copolymer composition for fast reforming were obtained.
  • the asphalt composition was prepared and its performance was evaluated. Table 2 shows the evaluation results of each property.
  • the (mouth) block copolymer was polymerized in the same manner as in Example 4 except that the amounts of styrene, 1,3-butadiene, sec-butyl lithium and ethylenedaryl glycol ether were changed.
  • the block copolymer composition shown in 2 and the block copolymer composition were obtained, an asphalt composition was prepared, and its performance was evaluated. Table 2 shows the evaluation results of each property.
  • the block copolymer shown in Table 2 and the block copolymer composition for reforming asphalt shown in Table 2 were prepared in the same manner as in Example 3 except that the amounts of styrene, 1,3-butadiene and sec-butyllithium were changed. An asphalt composition was prepared and its performance was evaluated. Table 2 shows the evaluation results of each property.
  • a block copolymer is obtained in the same manner as in Example 1 except that the charge of styrene, 1,3-butadiene, sec-butyllithium and ethylene glycol jettyl ether is changed, and an asphalt composition is prepared. The performance was evaluated. Table 3 shows the evaluation results of each property. In addition, a photomicrograph of the composition of Comparative Example 2 is shown in FIG. It can be seen that this asphalt composition remains in phase separation between the Bucock copolymer composition phase and asphalt.
  • a block copolymer was obtained, an asphalt composition was prepared, and its performance was evaluated in the same manner as in Example 3 except that the amounts of styrene, 1,3-butadiene and sec-butyllithium were changed. Table 3 shows the evaluation results of each property. 3 ⁇ 4 3
  • the asphalt composition of the present invention has a short dissolution time to asphalt, low melt viscosity, good storage stability, good toughness, tenacity, softening point and elongation. It can be seen that
  • Comparative Example 1 and Comparative Example 4 which are the asphalt composition which does not contain the block copolymer of the present invention have a long dissolution time, a high melt viscosity, and a storage stability. Poor sex.
  • Comparative Example 2 and Comparative Example 5 the molecular weight in the polymer block S of the block copolymer (i) to be added to the (mouth) block copolymer is outside the range of the present invention, and the dissolution time is long. The stability is also bad.
  • the blending amount of the block copolymer (i) of the present invention is large, and the softening point, toughness, tenacity and elongation are inferior.
  • Comparative Examples 6 to 10 are compositions comprising a copolymer outside the range of (i) block copolymer and (opening) block copolymer, and none of them can provide satisfactory physical properties. .
  • Example 12 is the same as Example 12 except that the amounts of styrene, 1,3-butadiene and sec-butyllithium are changed.
  • 60 g, penetration 70 straight asphalt [Co. petroleum, 6 0/80] 600 g with a stirrer while heating at 180 ° C.
  • Specialized An asphalt composition was prepared by mixing with an industrial company, TK homomixer, 10, OOO rpm]. Table 4 shows the evaluation results of each property.
  • Comparative example 1 1 The block copolymer composition shown in Table 4 obtained in the same manner as in Example 12 except that the amounts of styrene, 1,3-butadiene and sec_butyllithium were changed was the same as in Example 25. An asphalt composition was prepared by the method. Table 4 shows the evaluation results of each property.
  • An asphalt composition was prepared in the same manner as in Example 25 using the (mouth) block copolymer used in Example 25 with the composition shown in Table 4.
  • Table 4 shows the evaluation results of each property.
  • Bound styrene content (%) 31 31 31 31 31 31 31 31 31 polystyrene block (10,000) 1.55 1.55 1.55 1.55 1.55 1.55 1.55 1.55 block copolymer molecule ⁇ weight Mw (10,000) 18 18 18 18 18 18 18 Conjugating gent Vinyl content (.) 37 37 37 37 37 37 37 37 37 Alteration block copolymer composition
  • Streave asphalt (parts by weight) 100 100 100 100 100 100 100 100 100 100 100 Modification block copolymer composition (weight part) 10 10 10 10 10 8 8 8 Zero quality oil (zero) * 10 ⁇ 10 10 10 10 10 15 10 Aromatic Hydrocarbon Resin (parts by weight) 5 5 5 5 5 5 5 5 5 10 10 Characteristics of Asphalt Composition
  • Dissolution time method A (hour) 1.5 1.5 1.5 4 6 3.5 2 2 dissolution time method B (hour)-4 4 4>8> 8 5 softening point CO 97 96 97 96 99 90 77 79 penetration (l / 10 mm) 52 53 51 54 48 60 65 39 Toughness (N'm) 29 30 28 26 31 20 17 15 Tenacity One (N'm) 18 20 19 17 20 15 12 11 Elongation (1 5 ° C.) 95 98 97 92 99 75 67 65 Melt viscosity (Pa ⁇ s) 680 700 680 940 1100 650 580 600 Storage stability (surface covering condition) ⁇ ⁇ ⁇ XXX ⁇ ⁇ Difference in softening point after storage (upper layer-lower layer) ° C 0 0 0 17 25 15 1 0
  • Examples 25 to 27 are the asphalt compositions using an aromatic hydrocarbon resin and a heavy oil in combination within the scope of the present invention, which have a short dissolution time to asphalt and a melt viscosity Has a low viscosity, good storage stability, and good toughness, tenacity, softening point and elongation.
  • Comparative Example 1 1 of Table 4 the molecular weight of the polymer block of (i) is outside the range of the present invention, the dissolution time is long, and the storage stability is also poor.
  • Comparative Examples 1 to 15 are (2) an asphalt composition containing no block copolymer of the present invention, having poor dissolution time, softening point, penetration degree, toughness, tenacity, and balance of storage stability. In any case, satisfactory physical properties can not be obtained.
  • the (i) block (co) polymer of the present invention can easily compatibilize asphalt and an sulfanorete modifier containing as a main component a copolymer of an aromatic bule compound and a conjugated diene, and An optimum structure can also be designed according to the Asphalt and Asphalt modifiers, and is suitable as a compatibilizer.
  • the composition for modifying asphalts of the present invention is a composition of the (i) polymer of the present invention (co) polymer and an asphalt modifier, and is extremely excellent in solubility.
  • the asphalt composition By blending such a composition for reforming asphalt with straight asphalt etc., the asphalt composition with good toughness, tenacity, softening point and elongation property and good balance of the asphalt, and further, road pavement, waterproof sheet, sound insulation Seats, waterproofing materials, roofing materials, sealing materials, covering materials, covering materials, silencer sheets, steel pipe coatings, etc.
  • a falto composition can be obtained.

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Abstract

L'invention concerne une composition pour la modification d'asphalte qui comprend (i) un (co)polymère séquencé représenté par la formule générale (S-B)m-S'n (I) (dans laquelle S et S' représentent chacun un bloc polymère constitué essentiellement d'un composé vinyle aromatique ; B représente un bloc polymère constitué essentiellement d'un diène conjugué ; m et n représentent chacun 0 ou 1, à condition que m + n représente 1 ou davantage) et ayant une teneur de tous les composés vinyle aromatique combinés de 10 à 100 % en poids, 10 % en poids exclu, et (ii) au moins un ingrédient représenté par la formule générale S-B-S (II), la formule générale S-B-S' (III) et/ou la formule générale (S-B)2-X (IV) (dans les formules (II) à (IV), S, S' et B ont les mêmes significations que dans la formule générale (I) et X représente un résidu d'un agent de couplage), le rapport pondéral (i)/(ii) étant de (10-40)/(90-60) ; et une composition d'asphalte contenant de l'asphalte auquel est ajoutée la composition de modification. La composition de modification d'asphalte présente une excellente solubilité dans l'asphalte et une excellente stabilité de stockage à hautes températures, elle présente une viscosité à bas point de fusion et elle donne d'excellentes propriétés à l'asphalte. La composition d'asphalte est utilisable pour le revêtement de routes ou en tant que plaque étanche à l'eau.
PCT/JP2004/001923 2003-03-07 2004-02-19 (co)polymere sequence, composition de copolymere sequence pour la modification d'asphalte, leur procede de production et composition d'asphalte WO2004078812A1 (fr)

Priority Applications (5)

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BRPI0407647-8A BRPI0407647A (pt) 2003-03-07 2004-02-19 (co) polìmero de bloco, composição de copolìmero de bloco para a modificação de asfalto, processo para a produção do mesmo, e composição de asfalto
EP04712739A EP1602673A4 (fr) 2003-03-07 2004-02-19 (co)polymere sequence, composition de copolymere sequence pour la modification d'asphalte, leur procede de production et composition d'asphalte
CA2517142A CA2517142C (fr) 2003-03-07 2004-02-19 (co)polymere sequence, composition de copolymere sequence pour modification d'asphalte, procede pour leur production et composition d'asphalte
US10/545,552 US20060229391A1 (en) 2003-03-07 2004-02-19 Block (co) polymer, block copolymer composition for asphalt modification, process for producing the same, and asphalt composition
AU2004218190A AU2004218190B9 (en) 2003-03-07 2004-02-19 Block (co)polymer, block copolymer composition for asphalt modification, process for producing the same, and asphalt composition

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JP2003328390A JP4069389B2 (ja) 2003-03-07 2003-09-19 アスファルト改質用ブロック共重合体組成物、その製造方法、およびアスファルト組成物
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JP4145856B2 (ja) 2004-10-05 2008-09-03 ジヤトコ株式会社 ベルト式無段変速機のライン圧制御装置
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CN100448906C (zh) * 2006-08-10 2009-01-07 大连海事大学 端胺基和羧基苯乙烯/丁二烯共聚物的合成及其制备贮存稳定的改性沥青的方法
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KR100923535B1 (ko) * 2007-11-21 2009-10-27 금호석유화학 주식회사 테이퍼드된 블록 공중합체를 함유한 개질 아스팔트 조성물
CN101981121B (zh) * 2008-03-31 2013-02-06 日本瑞翁株式会社 嵌段共聚物组合物、其制备方法及薄膜
KR20100009799A (ko) * 2008-07-21 2010-01-29 주식회사 엘지화학 아스팔트 개질제 조성물 및 이를 함유하는 아스팔트 조성물
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US8324309B2 (en) * 2010-04-27 2012-12-04 Kraton Polymers Us Llc High melt flow block copolymers for non-woven adhesives
JP5615679B2 (ja) * 2010-11-29 2014-10-29 昭和シェル石油株式会社 ポリマー改質アスファルト組成物
JP5671131B1 (ja) * 2013-12-27 2015-02-18 昭和シェル石油株式会社 スチレン−ブタジエン系添加剤
KR102081769B1 (ko) * 2016-10-21 2020-02-26 주식회사 엘지화학 아스팔트 개질제 및 이를 포함하는 아스팔트 조성물
KR101984725B1 (ko) * 2016-10-21 2019-05-31 주식회사 엘지화학 아스팔트 개질제 및 이를 포함하는 아스팔트 조성물
JP2024532322A (ja) * 2021-08-27 2024-09-05 花王株式会社 アスファルト組成物
JP7396761B1 (ja) * 2023-08-23 2023-12-12 大有建設株式会社 アスファルト改質材とこれを使用したアスファルト混合物

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AU2004218190B9 (en) 2009-03-05
TW200424258A (en) 2004-11-16
TWI336341B (fr) 2011-01-21
AU2004218190B2 (en) 2009-02-05
US20060229391A1 (en) 2006-10-12
BRPI0407647A (pt) 2006-02-21
KR101005957B1 (ko) 2011-01-05
EP1602673A1 (fr) 2005-12-07
JP4069389B2 (ja) 2008-04-02
KR20050106088A (ko) 2005-11-08
CA2517142C (fr) 2012-06-26
EP1602673A4 (fr) 2008-06-18
CA2517142A1 (fr) 2004-09-16
AU2004218190A1 (en) 2004-09-16

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